JPH0770228A - Production of water absorbing resin - Google Patents

Production of water absorbing resin

Info

Publication number
JPH0770228A
JPH0770228A JP21764793A JP21764793A JPH0770228A JP H0770228 A JPH0770228 A JP H0770228A JP 21764793 A JP21764793 A JP 21764793A JP 21764793 A JP21764793 A JP 21764793A JP H0770228 A JPH0770228 A JP H0770228A
Authority
JP
Japan
Prior art keywords
water
absorbent resin
resin powder
drying
absorbing resin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP21764793A
Other languages
Japanese (ja)
Other versions
JP2898180B2 (en
Inventor
Masunori Ozaki
益教 尾崎
Akio Ikeda
明夫 池田
Takao Honmochi
隆夫 本持
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sekisui Kasei Co Ltd
Original Assignee
Sekisui Plastics Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sekisui Plastics Co Ltd filed Critical Sekisui Plastics Co Ltd
Priority to JP21764793A priority Critical patent/JP2898180B2/en
Publication of JPH0770228A publication Critical patent/JPH0770228A/en
Application granted granted Critical
Publication of JP2898180B2 publication Critical patent/JP2898180B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Processes Of Treating Macromolecular Substances (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

PURPOSE:To obtain the subject resin excellent in water absorption rate and gel strength and useful for sanitary goods, etc., by adding untreated water- absorbing resin powder during drying after adding a treating liquid containing water, a dispersing agent and a crosslinkinga gent or immediately after finishing drying in treating the water-absorbing resin powder with the treating liquid. CONSTITUTION:In treating (B) a water-absorbing resin powder with (A) a treating liquid consisting of water, a dispersing agent and a crosslinking agent, during drying after adding the treating liquid A or immediately after finishing drying,(C) untreated water-absorbing resin powder is added thereto to provide the objective resin. Furthermore, when the objective resin is obtained, the water- absorbing resin used is a polyacrylic acid (co)polymer, etc., and the particle diameter has 5-400 mesh based on Tyler standard sieve. In the treating liquid A, amounts of components used based on 100 pts.wt. of the waterabsorbing resin are as follows. The crosslinking agent: 0.005-5 pts.wt.; the dispersing agent: 0.05-10 pts.wt.; water: 1-50 pts.wt.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は吸水性樹脂の製造方法に
関する。
FIELD OF THE INVENTION The present invention relates to a method for producing a water absorbent resin.

【0002】[0002]

【従来の技術】吸水性樹脂は高い吸水量を有し、保水力
にも優れていることから、おむつ、生理用品などの衛生
用品はもとより、農業、園芸、食品、医薬などの分野で
も広く使用されている。一般に、吸水性樹脂には、高い
吸水量と保水力のほかに、高いゲル強度を有することが
要求される。吸水性樹脂のゲル強度が弱いと、例えばお
むつ製品の場合、含水ゲルが糊状となり、乳児の体重と
動きにより型崩れを起こし、おむつ漏れの原因となる場
合がある。さらに、ゲル強度が弱いと、含水ゲルのべと
つきが大きく、ウェットバックが悪くなり、おむつの品
質が悪くなる。
2. Description of the Related Art Since water-absorbent resins have a high water absorption capacity and excellent water retention ability, they are widely used not only in hygiene products such as diapers and sanitary products but also in fields such as agriculture, gardening, food and medicine. Has been done. Generally, a water absorbent resin is required to have high gel strength in addition to high water absorption and water retention. When the gel strength of the water-absorbent resin is weak, for example, in the case of diaper products, the water-containing gel becomes pasty, and the baby may lose its shape due to the weight and movement of the baby, which may cause diaper leakage. Further, when the gel strength is weak, the water-containing gel becomes large in stickiness, the wet back is deteriorated, and the quality of the diaper is deteriorated.

【0003】そのため、従来より、二次処理として、吸
水性樹脂粉末の表面に処理を施してゲル強度を大きくす
ることが行われている。すなわち、特開昭58−426
02号公報には、水酸基またはカルボキシル基を有する
親水性架橋重合体を、メタノール、エタノールなどの分
散媒に分散させ、多価金属塩等の架橋剤で表面を架橋し
て、吸水速度およびゲル強度を高めることが開示されて
いる。
Therefore, conventionally, as a secondary treatment, the surface of the water-absorbent resin powder is treated to increase the gel strength. That is, JP-A-58-426
No. 02 publication discloses that a hydrophilic crosslinked polymer having a hydroxyl group or a carboxyl group is dispersed in a dispersion medium such as methanol or ethanol, and the surface is crosslinked with a crosslinking agent such as a polyvalent metal salt to obtain a water absorption rate and gel strength. Is disclosed.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、上記の
ような二次処理は、攪拌混合工程と乾燥工程とを必要と
するため、その処理能力に限界があった。そのため、全
ての吸水性樹脂に二次処理を施すことは処理能力のうえ
で困難であった。そこで、未処理吸水性樹脂粉末(一次
処理品)を、二次処理した吸水性樹脂粉末(二次処理
品)に混合することが提案されているが、混合して得ら
れる吸水性樹脂はゲル強度などの品質が二次処理品に比
べて非常に劣るため、実用に供することができなかっ
た。
However, the secondary treatment as described above requires a stirring and mixing step and a drying step, and thus has a limited processing capacity. Therefore, it is difficult to perform the secondary treatment on all the water-absorbent resins in terms of treatment capacity. Therefore, it has been proposed to mix the untreated water-absorbent resin powder (primary treatment product) with the secondary-treated water-absorbent resin powder (secondary treatment product). Since the strength and other qualities are extremely inferior to those of the secondary treated product, they could not be put to practical use.

【0005】本発明の主たる目的は、二次処理の負担を
軽減し、かつ実使用が可能な品質を有する吸水性樹脂の
製造方法を提供することである。
A main object of the present invention is to provide a method for producing a water-absorbent resin which has a quality capable of reducing the burden of secondary treatment and being practically used.

【0006】[0006]

【課題を解決するための手段および作用】上述の技術的
課題を解決するために、本発明者らは鋭意研究を重ねた
結果、未処理吸水性樹脂粉末(一次処理品)と、二次処
理した吸水性樹脂粉末(二次処理品)とを単に混合する
のではなく、二次処理工程における処理液添加後の乾燥
中または乾燥終了直後に、未処理吸水性樹脂粉末を添加
し攪拌混合するときは、実使用が可能な高い品質を有す
る吸水性樹脂が得られるという新たな知見を得て、本発
明を完成するに到った。
Means and Actions for Solving the Problems In order to solve the above technical problems, the inventors of the present invention have conducted extensive studies, and as a result, untreated water-absorbent resin powder (primary treatment product) and secondary treatment The above-mentioned water-absorbent resin powder (secondary treated product) is not simply mixed, but the untreated water-absorbent resin powder is added and stirred and mixed during the drying after the treatment liquid addition in the secondary treatment step or immediately after the drying. At this time, new knowledge that a water-absorbent resin having a high quality that can be actually used can be obtained, and the present invention has been completed.

【0007】すなわち、本発明の吸水性樹脂の製造方法
は、水、分散剤および架橋剤からなる処理液にて吸水性
樹脂粉末を処理するにあたり、前記処理液添加後の乾燥
中または乾燥終了直後に、未処理吸水性樹脂粉末を添加
することを特徴とする。かかる本発明によれば、二次処
理した吸水性樹脂粉末に一次処理品である未処理吸水性
樹脂粉末を混合するので、吸水性樹脂粉末の二次処理量
を低減でき、二次処理の負担が軽減する。また、得られ
た吸水性樹脂はゲル強度などの品質が二次処理品と同等
か、あるいは殆ど変わらない程度であるので、充分に実
使用が可能である。
That is, in the method for producing a water-absorbent resin of the present invention, when the water-absorbent resin powder is treated with a treatment liquid consisting of water, a dispersant and a cross-linking agent, during the drying after the treatment liquid is added or immediately after the drying is finished. In addition, untreated water-absorbent resin powder is added. According to the present invention, since the untreated water-absorbent resin powder, which is the primary treated product, is mixed with the secondary-treated water-absorbent resin powder, the secondary treatment amount of the water-absorbent resin powder can be reduced, and the burden of the secondary treatment can be reduced. Is reduced. In addition, the obtained water-absorbent resin has a quality such as gel strength which is equal to or almost the same as that of the secondary treated product, and thus can be sufficiently practically used.

【0008】本発明において使用される吸水性樹脂とし
ては、従来より使用されている種々の吸水性樹脂、例え
ば架橋ポリエチレンオキシド、架橋ポリビニルアルコー
ル、架橋型ポリアクリル酸およびその塩、セルロース−
アクリル酸グラフト共重合体およびその塩、澱粉−アク
リロニトリルグラフト共重合体の加水分解物などがあげ
られ、とくにカルボキシル基および/またはカルボキシ
レート部分を有する重合体、例えば主鎖にアクリル酸ま
たはアクリル酸塩のモノマー単位を有する重合体または
共重合体からなるポリアクリル酸系の吸水性樹脂を使用
するのが好ましい。
As the water absorbent resin used in the present invention, various conventionally used water absorbent resins such as crosslinked polyethylene oxide, crosslinked polyvinyl alcohol, crosslinked polyacrylic acid and its salts, and cellulose-
Examples thereof include acrylic acid graft copolymers and salts thereof, and hydrolysates of starch-acrylonitrile graft copolymers. Particularly, polymers having a carboxyl group and / or a carboxylate moiety, such as acrylic acid or acrylate in the main chain. It is preferable to use a polyacrylic acid-based water-absorbent resin composed of a polymer or copolymer having the monomer unit (1).

【0009】かかるポリアクリル酸系の重合体として
は、例えばポリアクリル酸、ポリアクリル酸塩、アクリ
ル酸とアクリル酸塩との共重合体等があげられる。ここ
で、ポリアクリル酸塩およびアクリル酸塩の塩部分とし
ては、ナトリウム塩、カリウム塩などのアルカリ金属
塩、アンモニウム塩等の有機塩基塩をあげることができ
る。また、親水性等の特性を改良するために、主鎖にア
クリル酸またはアクリル酸塩のモノマー単位を有する重
合体とアクリルアミド、N−ビニルピロリドン、2−ヒ
ドロキシエチルメタクリレート等との共重合体であって
もよい。
Examples of such polyacrylic acid-based polymers include polyacrylic acid, polyacrylic acid salts, and copolymers of acrylic acid and acrylic acid salts. Here, examples of the polyacrylic acid salt and the salt portion of the acrylic acid salt include alkali metal salts such as sodium salt and potassium salt, and organic base salts such as ammonium salt. Further, in order to improve properties such as hydrophilicity, it is a copolymer of a polymer having a monomer unit of acrylic acid or acrylate in its main chain and acrylamide, N-vinylpyrrolidone, 2-hydroxyethyl methacrylate or the like. May be.

【0010】また、吸水性樹脂は架橋したものが好まし
く、架橋に際しては公知の架橋手段を用いることができ
る。例えばN−メチロールアクリルアミド等の架橋性モ
ノマーとの共重合体を加熱したり、ペルオキソ硫酸カリ
ウム等の酸化性を有する触媒を用いることにより、ある
いは2個以上の重合性不飽和結合を有するN,N’−メ
チレンビスアクリルアミド、エチレングリコールジアク
リレート等の架橋剤を重合の際に添加したりして架橋す
ることができる。
The water-absorbent resin is preferably cross-linked, and known cross-linking means can be used for cross-linking. For example, by heating a copolymer with a cross-linking monomer such as N-methylol acrylamide, by using an oxidizing catalyst such as potassium peroxosulfate, or by using N, N having two or more polymerizable unsaturated bonds. It is possible to crosslink by adding a crosslinking agent such as'-methylenebisacrylamide, ethylene glycol diacrylate during the polymerization.

【0011】通常はアクリル酸またはアクリル酸塩の水
溶液に、必要に応じて他の共重合性モノマーおよび上記
の架橋剤を添加して重合させる方法が採用されている。
この方法で得られる重合体は乾燥すると塊状に固化する
ので、高吸水性樹脂素材に適した大きさの粒径に粉砕機
を用いて粉砕する。なお、乳化重合または懸濁重合によ
り得られる重合体は小さな球状をなしているので、その
まま用いてもよく、さらに粉砕して微細化して用いても
よい。
Usually, a method is adopted in which, if necessary, another copolymerizable monomer and the above-mentioned crosslinking agent are added to an aqueous solution of acrylic acid or an acrylic acid salt to carry out polymerization.
Since the polymer obtained by this method solidifies into a lump when dried, it is pulverized using a pulverizer into a particle size of a size suitable for a super absorbent polymer material. Since the polymer obtained by emulsion polymerization or suspension polymerization has a small spherical shape, it may be used as it is, or may be further pulverized into fine particles before use.

【0012】かくして得られる吸水性樹脂粉末(一次処
理品)の粒径は、タイラー標準篩において5〜400メ
ッシュ品が好ましく、16〜150メッシュ品(110
〜1000μm)がより好ましい。吸水性樹脂粉末の二
次処理を行うための処理液は、水、分散剤および架橋剤
からなる。
The water-absorbent resin powder (primary treated product) thus obtained preferably has a particle size of 5 to 400 mesh, preferably 16 to 150 mesh (110) on a Tyler standard sieve.
˜1000 μm) is more preferable. The treatment liquid for carrying out the secondary treatment of the water absorbent resin powder comprises water, a dispersant and a crosslinking agent.

【0013】分散液は、二次処理の際に凝集によるダマ
が発生するのを防止し、均一な架橋処理を行うために使
用される。かかる分散液としては、例えばジエチレング
リコールメチルエーテル、ジエチレングリコールエチル
エーテル、ジエチレングリコールジエチルエーテル、ジ
エチレングリコールジブチルエーテル、プロピレングリ
コールメチルエーテル、プロピレングリコールエチルエ
ーテル、ジプロピレングリコールメチルエーテル、ジプ
ロピレングリコールエチルエーテル、トリプロピレング
リコールメチルエーテル、テトラエチレングリコールジ
メチルエーテルなどのエーテル化合物;ブタンジオール
(例えば1,2−ブタンジオール、1,3−ブタンジオ
ール、1,4−ブタンジオール、2,3−ブタンジオー
ル)、ペンタンジオール(例えば1,5−ペンタンジオ
ール、1,3−ペンタンジオール、2,3−ペンタンジ
オール)、ヘキサンジオール(例えば1,6−ヘキサン
ジオール、2,5−ヘキサンジオール)、2−メチル−
2,4−ペンタンジオール、2−メチル−2,3−ブタ
ンジオールなどの炭素数4〜6の二価アルコールなどが
あげられる。分散剤の使用量は、吸水性樹脂100重量
部に対して0.05〜10重量部であるのが好ましい。
また、水100重量部に対しては2〜50重量部である
のが好ましい。
The dispersion is used to prevent the generation of lumps due to aggregation during the secondary treatment and to carry out a uniform crosslinking treatment. Such dispersions include, for example, diethylene glycol methyl ether, diethylene glycol ethyl ether, diethylene glycol diethyl ether, diethylene glycol dibutyl ether, propylene glycol methyl ether, propylene glycol ethyl ether, dipropylene glycol methyl ether, dipropylene glycol ethyl ether, tripropylene glycol methyl ether. An ether compound such as tetraethylene glycol dimethyl ether; butanediol (eg, 1,2-butanediol, 1,3-butanediol, 1,4-butanediol, 2,3-butanediol), pentanediol (eg, 1,5) -Pentanediol, 1,3-pentanediol, 2,3-pentanediol), hexanediol Such as 1,6-hexanediol, 2,5-hexanediol), 2-methyl -
Examples thereof include dihydric alcohols having 4 to 6 carbon atoms such as 2,4-pentanediol and 2-methyl-2,3-butanediol. The amount of the dispersant used is preferably 0.05 to 10 parts by weight with respect to 100 parts by weight of the water absorbent resin.
Further, it is preferably 2 to 50 parts by weight with respect to 100 parts by weight of water.

【0014】また、水を添加するのは、二次処理におけ
る架橋深度、すなわち吸水性樹脂の架橋部分の表面から
の深さを均一化するためである。水の添加量は、吸水性
樹脂100重量部に対して1〜50重量部であるのが好
ましい。また、これらの水および分散剤と共に添加され
る架橋剤は、前記吸水性樹脂と反応しうる2個以上の官
能基を有するものである。かかる架橋剤としては、とく
に吸水性樹脂が有するカルボキシル基またはカルボキシ
レート部分と反応しうるものであればよく、例えばアル
デヒド化合物(グルタルアルデヒド、グリオキザールな
ど)、イソシアネート化合物(例えば2,4−トリレン
ジイソシアネート、ヘキサメチレンジイソシアネートな
ど)、ハロエポキシ化合物(例えばエピクロルヒドリ
ン、エピブロモヒドリンなど)、エポキシ化合物(例え
ばエチレングリコールジグリシジルエーテル、ジエチレ
ングリコールジグリシジルエーテル、ポリエチレングリ
コールジグリシジルエーテル、プロピレングリコールジ
グリシジルエーテル、ジプロピレングリコールジグリシ
ジルエーテル、ポリプロピレングリコールジグリシジル
エーテル、グリセリンジグリシジルエーテル、ポリグリ
セリンポリグリシジルエーテル、ペンタエリトリトール
ポリグリシジルエーテル、ソルビトールポリグリシジル
エーテルなど)、多価の金属化合物などをあげることが
できる。これらの架橋剤のうち、エポキシ化合物および
アルミニウム塩とアルミン酸塩またはアルミニウム塩と
アルカリ金属水酸化物との反応によって得られる水酸化
アルミニウムゲル(特開昭62−25072号公報を参
照)を使用するのが好ましい。
Water is added in order to make the cross-linking depth in the secondary treatment, that is, the depth from the surface of the cross-linked portion of the water absorbent resin uniform. The amount of water added is preferably 1 to 50 parts by weight with respect to 100 parts by weight of the water absorbent resin. The cross-linking agent added together with these water and dispersant has two or more functional groups capable of reacting with the water-absorbent resin. Such a cross-linking agent may be one that can react particularly with a carboxyl group or a carboxylate moiety of the water absorbent resin, and examples thereof include aldehyde compounds (glutaraldehyde, glyoxal, etc.), isocyanate compounds (for example, 2,4-tolylene diisocyanate). , Hexamethylene diisocyanate, etc., haloepoxy compound (eg epichlorohydrin, epibromohydrin etc.), epoxy compound (eg ethylene glycol diglycidyl ether, diethylene glycol diglycidyl ether, polyethylene glycol diglycidyl ether, propylene glycol diglycidyl ether, dipropylene glycol) Diglycidyl ether, polypropylene glycol diglycidyl ether, glycerin diglycidyl ether, Li glycerol polyglycidyl ether, pentaerythritol polyglycidyl ether, sorbitol polyglycidyl ether), and the like polyvalent metal compounds. Among these crosslinking agents, an epoxy compound and an aluminum hydroxide gel obtained by the reaction of an aluminum salt with an aluminate or an aluminum salt with an alkali metal hydroxide (see JP-A-62-25072) are used. Is preferred.

【0015】これらの架橋剤の添加量は、求める吸水特
性、ゲル強度等に応じて適宜決定することができるが、
通常、吸水性樹脂100重量部に対して0.001〜1
0重量部、好ましくは0.005〜5重量部の割合で用
いられる。二次処理方法としては、種々の方法があげら
れるが、一般には、混合機に吸水性樹脂粉末を収容し、
これに分散剤と架橋剤とを水に溶解または分散させた処
理液を攪拌しながら滴下またはスプレーし、充分に混合
して架橋処理した後、乾燥機で乾燥する方法などが採用
される。
The amount of these cross-linking agents added can be appropriately determined according to the desired water absorption characteristics, gel strength and the like.
Usually, 0.001 to 1 per 100 parts by weight of the water absorbent resin
It is used in an amount of 0 part by weight, preferably 0.005 to 5 parts by weight. Examples of the secondary treatment method include various methods. Generally, a water-absorbent resin powder is stored in a mixer,
A method in which a treatment liquid in which a dispersant and a cross-linking agent are dissolved or dispersed in water is dropped or sprayed with stirring, sufficiently mixed to perform cross-linking treatment, and then dried with a drier is used.

【0016】使用する混合機はとくに限定されず、ナウ
ターミキサー、リボンブレンダー、コニカルブレンダ
ー、ヘンシェルミキサー、ライカイ器などの混合機がい
ずれも使用可能である。また、処理後に行う乾燥に際し
ても、通常の乾燥機、例えば熱風循環乾燥機、減圧乾燥
機などがいずれも使用可能である。乾燥温度は室温〜1
50℃、好ましくは90〜140℃であり、かつ乾燥時
間は含水率が1〜7%になるように設定するのが好まし
い。
The mixer to be used is not particularly limited, and any mixer such as a Nauter mixer, ribbon blender, conical blender, Henschel mixer, and Raikai mixer can be used. Also, for the drying performed after the treatment, any ordinary dryer such as a hot air circulating dryer or a vacuum dryer can be used. Drying temperature is room temperature to 1
It is preferably 50 ° C., preferably 90 to 140 ° C., and the drying time is preferably set so that the water content is 1 to 7%.

【0017】本発明においては、前記処理液添加後の乾
燥中または乾燥終了直後に、未処理吸水性樹脂粉末を添
加し攪拌混合する。ただし、乾燥中の未処理吸水性樹脂
粉末の添加は、乾燥終了後の冷却に時間が必要であるた
め、乾燥終了直後に未処理吸水性樹脂粉末を添加するの
が好ましい。ここで、乾燥終了直後とは、乾燥機から取
り出した製品の温度が殆ど下がらないまでの時間をい
い、具体的には製品の温度が5℃以上下がらないまでの
時間である。
In the present invention, the untreated water-absorbent resin powder is added and stirred and mixed during the drying after the addition of the treatment liquid or immediately after the completion of the drying. However, the addition of the untreated water-absorbent resin powder during drying requires time for cooling after the completion of drying, so it is preferable to add the untreated water-absorbent resin powder immediately after the completion of drying. Here, the term “immediately after completion of drying” refers to the time until the temperature of the product taken out from the dryer hardly decreases, specifically, the time until the temperature of the product does not decrease by 5 ° C. or more.

【0018】未処理吸水性樹脂粉末との攪拌は、開放状
態で行ってもよいが、密閉状態で行うほうが、未処理吸
水性樹脂を混合して得られる吸水性樹脂の品質が高くな
るので好ましい。その理由は明らかではないが、処理液
の蒸気が未処理吸水性樹脂に吸収され、二次処理効果を
発揮するためではないかと考えられる。密閉状態で攪拌
混合するには、例えばスーパーミキサーに処理品を入
れ、蓋をして加熱、攪拌混合すればよい。
The stirring with the untreated water-absorbent resin powder may be performed in an open state, but it is preferable to perform the stirring in a closed state because the quality of the water-absorbent resin obtained by mixing the untreated water-absorbent resin is improved. . The reason for this is not clear, but it is considered that this is because the vapor of the treatment liquid is absorbed by the untreated water-absorbent resin to exert the secondary treatment effect. In order to stir and mix in a closed state, for example, the treated product may be put in a super mixer, covered and heated to stir and mix.

【0019】また、処理後の冷却された二次処理品を加
熱して、これに未処理の吸水性樹脂を混合しても、得ら
れる製品は品質が劣っており、かつ加熱を必要とするの
で好ましくない。一方、未処理の吸水性樹脂をあらかじ
め加えて二次処理を行っても、品質は充分でない。乾燥
中または乾燥終了直後における未処理吸水性樹脂粉末の
添加量は、二次処理吸水性樹脂粉末100重量部に対し
て10〜500重量部、好ましくは50〜150重量部
である。未処理吸水性樹脂粉末の添加量が10重量部よ
り少ないときは、実質的に二次処理品だけの製品と変わ
らず、二次処理の負担を軽減することにならない。一
方、未処理吸水性樹脂粉末の添加量が500重量部を超
えるときは、ゲル強度などの品質が劣ったものになる。
Even if the cooled secondary treated product after the treatment is heated and the untreated water-absorbent resin is mixed therein, the obtained product is inferior in quality and requires heating. It is not preferable. On the other hand, the quality is not sufficient even if the untreated water-absorbent resin is added in advance to carry out the secondary treatment. The amount of the untreated water-absorbent resin powder added during or immediately after the drying is 10 to 500 parts by weight, preferably 50 to 150 parts by weight, based on 100 parts by weight of the secondary treated water-absorbent resin powder. When the amount of the untreated water-absorbent resin powder added is less than 10 parts by weight, it is substantially the same as the secondary treated product, and the burden of the secondary treatment cannot be reduced. On the other hand, when the amount of untreated water-absorbent resin powder added exceeds 500 parts by weight, the quality such as gel strength becomes poor.

【0020】なお、処理液の添加量を一定にして未処理
吸水性樹脂粉末の添加量を増大させると、ゲル強度が低
下するので、未処理吸水性樹脂粉末の添加量が多いとき
は、処理液の添加量もそれに応じて増大させるのが好ま
しい。二次処理吸水性樹脂粉末と未処理吸水性樹脂粉末
との攪拌混合は、未処理吸水性樹脂粉末の添加が乾燥終
了直後の場合には、そのまま前記した混合機を使用して
2〜5分間行えばよい。また、乾燥中の場合は乾燥後の
攪拌混合はとくに必要はないが、均一な混合を行ううえ
で混合処理を行うのが好ましい。
When the amount of untreated water-absorbent resin powder added is increased while the amount of treated liquid added is kept constant, the gel strength decreases. It is preferable to increase the amount of the liquid added accordingly. The secondary treated water-absorbent resin powder and the untreated water-absorbent resin powder are mixed by stirring for 2 to 5 minutes by using the above-mentioned mixer as they are, when the addition of the untreated water-absorbent resin powder is immediately after the completion of drying. Just go. In addition, when drying is in progress, stirring and mixing after drying are not particularly necessary, but it is preferable to perform a mixing treatment for uniform mixing.

【0021】[0021]

【実施例】【Example】

参考例(未処理吸水性樹脂粉末の調製) 80%アクリル酸水溶液75.0重量部、48.6%水
酸化ナトリウム水溶液54.9重量部、脱イオン水5
6.1重量部を混合し、中和度80%のモノマー水溶液
を調製した。
Reference Example (Preparation of untreated water absorbent resin powder) 80% acrylic acid aqueous solution 75.0 parts by weight, 48.6% sodium hydroxide aqueous solution 54.9 parts by weight, deionized water 5
6.1 parts by weight were mixed to prepare an aqueous monomer solution having a neutralization degree of 80%.

【0022】次に、得られたモノマー水溶液1023g
に1%N,N’−メチレンビスアクリルアミド水溶液1
5gを添加した後、窒素ガスにて溶存酸素を置換した。
ついで、1%過硫酸カリウム33g、1%ピロ亜硫酸カ
リウム40gおよび0.04%グリオキザール水溶液2
5gを順次15秒かけて投入混合した。なお、上記の
0.04%グリオキザール水溶液は、グリオキザール
(40%水溶液、日本合成化学社製)を水で100倍に
希釈したものである。
Next, 1023 g of the obtained monomer aqueous solution
1% N, N'-methylenebisacrylamide aqueous solution
After adding 5 g, the dissolved oxygen was replaced with nitrogen gas.
Then, 33% of 1% potassium persulfate, 40 g of 1% potassium pyrosulfite and 0.04% aqueous solution of glyoxal 2
5 g were sequentially added and mixed over 15 seconds. The 0.04% aqueous solution of glyoxal was obtained by diluting glyoxal (40% aqueous solution, manufactured by Nippon Synthetic Chemical Industry Co., Ltd.) 100 times with water.

【0023】得られた混合液を縦15cm、横20cm、高
さ4cmの箱形容器(SUS製、内面テトラフルオロエチ
レン樹脂加工)に注入し、温度35℃のウォーターバス
を用いて重合を行わせ、含水ゲルを得た。この含水ゲル
をドラムドライヤーで乾燥してフレーク状とし、これを
ピンミルで粉砕してアクリル酸−アクリル酸塩共重合体
架橋物からなる平均粒径42メッシュの吸水性樹脂粉末
(一次処理品)を得た。 実施例1〜7 (1) 二次処理用処理液の調製 水10gに、分散剤としてジエチレングリコールモノエ
チルエーテル1g、架橋剤としてエチレングリコールジ
グリシジルエーテル0.1gを溶解させて処理液を得
た。 (2) 二次処理 参考例で得た一次処理品100gを小型攪拌機に入れ、
攪拌しながら前記処理液の全量を噴霧して添加し、さら
に2分間攪拌した後、含水率が約7%になるように14
0℃の温度で乾燥した。乾燥直後の樹脂が熱いままの状
態で小型攪拌機に入れ、さらに前記一次処理品を表1に
示す量でそれぞれ添加し、開放状態および密閉状態のい
ずれかで3分間攪拌混合した。かくして得られた各実施
例の吸水性樹脂について、ゲル強度を測定した。その結
果を表1に併せて示す。 (ゲル強度の測定方法)100mlのビーカーに0.9
%食塩水60gを加え、マグネットスターラーで攪拌し
ながら、吸水性樹脂2gを添加してゲル化させた。生成
したゲルを8時間放置した後、カードメーター(飯尾電
機(株)製)を用いてゲルの硬さを測定した。
The obtained mixed solution was poured into a box-shaped container (15 cm in length, 20 cm in width, 4 cm in height) (made of SUS, inner surface treated with tetrafluoroethylene resin), and polymerization was carried out using a water bath at a temperature of 35 ° C. A hydrogel was obtained. This hydrogel is dried with a drum dryer to form flakes, which are pulverized with a pin mill to obtain a water-absorbent resin powder (primary treated product) having an average particle size of 42 mesh, which is composed of a cross-linked acrylic acid-acrylate copolymer. Obtained. Examples 1 to 7 (1) Preparation of treatment liquid for secondary treatment 1 g of diethylene glycol monoethyl ether as a dispersant and 0.1 g of ethylene glycol diglycidyl ether as a crosslinking agent were dissolved in 10 g of water to obtain a treatment liquid. (2) Secondary treatment Put 100 g of the primary treated product obtained in the reference example in a small stirrer,
While stirring, the whole amount of the treatment liquid was sprayed and added, and after stirring for another 2 minutes, the water content was adjusted to about 7%.
It was dried at a temperature of 0 ° C. The resin immediately after drying was placed in a small stirrer while still hot, and the above-mentioned primary treated products were further added in the amounts shown in Table 1, and the mixture was stirred and mixed for 3 minutes in either an open state or a closed state. The gel strength of the water-absorbent resin thus obtained in each example was measured. The results are also shown in Table 1. (Method of measuring gel strength) 0.9 in a 100 ml beaker
% Saline 60 g was added, and 2 g of the water-absorbent resin was added while stirring with a magnetic stirrer to cause gelation. After allowing the generated gel to stand for 8 hours, the hardness of the gel was measured using a card meter (manufactured by Iio Denki Co., Ltd.).

【0024】[0024]

【表1】 [Table 1]

【0025】表1から、一次処理品の配合量が多くなる
に従ってゲル強度は低下するものの、各実施例で得た吸
水性樹脂は、いずれも高いゲル強度を有していることが
わかる。また、実施例3と7との比較から、開放状態よ
りも密閉状態で攪拌混合したほうが高いゲル強度が得ら
れている。 比較例1〜6 参考例で得た一次処理品を実施例1〜7と同様にして処
理し、乾燥後、一次処理品を添加せずに放冷し、二次処
理品を得た。ついで、充分に放冷された二次処理品10
0gと一次処理品の表2に示す量とをそれぞれ小型攪拌
機に入れ、3分間攪拌混合した。かくして得られた各比
較例の吸水性樹脂について、前記と同様にしてゲル強度
を測定した。その結果を表2に併せて示す。なお、二次
処理品の樹脂温度は26℃であった。
It can be seen from Table 1 that the water-absorbent resins obtained in the respective examples have high gel strength, although the gel strength decreases as the blending amount of the primary treated product increases. Further, from the comparison between Examples 3 and 7, a higher gel strength is obtained by stirring and mixing in the closed state than in the open state. Comparative Examples 1 to 6 The primary treated products obtained in Reference Examples were treated in the same manner as in Examples 1 to 7, dried and then left to cool without adding the primary treated products to obtain secondary treated products. Then, the secondary treated product 10 that has been sufficiently cooled.
0 g and the amount of the primary treated product shown in Table 2 were placed in a small stirrer and mixed with stirring for 3 minutes. With respect to the water absorbent resin of each comparative example thus obtained, the gel strength was measured in the same manner as described above. The results are also shown in Table 2. The resin temperature of the secondary treated product was 26 ° C.

【0026】[0026]

【表2】 [Table 2]

【0027】表2から、比較例2〜5のように、単に一
次処理品と二次処理品とを混合するだけでは、比較例6
の一次処理品単独の場合に比べてゲル強度は向上するも
のの、比較例1の二次処理品単独の場合に比べてゲル強
度が著しく低下することがわかる。 実施例8〜9および比較例7〜9 参考例で得た一次処理品を表3に示す量でかつ同表に示
す処理液で実施例1〜7と同様にして処理し、同表に示
す一次処理品を攪拌混合した。かくして得られた各実施
例および比較例の吸水性樹脂について、ゲル強度を前記
と同様にして測定した。その結果を表3に併せて示す。
From Table 2, as in Comparative Examples 2 to 5, Comparative Example 6 is obtained by simply mixing the primary treated product and the secondary treated product.
It can be seen that the gel strength is improved as compared with the case of the primary treatment product alone, but the gel strength is significantly reduced as compared with the case of the secondary treatment product of Comparative Example 1 alone. Examples 8 to 9 and Comparative Examples 7 to 9 The primary treated products obtained in Reference Examples were treated in the amounts shown in Table 3 and with the treatment liquids shown in the same table as in Examples 1 to 7, and shown in the same table. The primary treated product was mixed by stirring. With respect to the water absorbent resins of the respective Examples and Comparative Examples thus obtained, the gel strength was measured in the same manner as described above. The results are also shown in Table 3.

【0028】[0028]

【表3】 [Table 3]

【0029】実施例3,8,9のように、乾燥直後に一
次処理品を混合するときは、比較例7〜9のように一次
処理品をあらかじめ混合しておくよりも、同じ処理液量
で高いゲル強度が得られることがわかる。また、実施例
8,9における一次処理品の添加量は実施例3よりも高
いにもかかわらず、処理液の使用量を実施例3のそれよ
りも多くすることにより、ゲル強度が低下するのが防止
されている。 実施例10〜12および比較例10〜11 参考例で得た一次処理品2kgをジャケット付小型攪拌
機(容量:10リットル)に入れ、攪拌しながら処理液
(水200g、ジエチレングリコールモノエチルエーテ
ル20gおよびエチレングリコールジグリシジルエーテ
ル2gを混合溶解したもの)を噴霧して添加した後、さ
らに3分間攪拌した。ついで、含水率が約7%になるよ
うに攪拌機のジャケットに蒸気を入れ、開放状態にて1
00℃で乾燥した。乾燥には25分間必要であった。こ
れらの工程の間、表4に示す各段階でそれぞれ一次処理
品2kgを添加した。乾燥終了後、各試料の条件を一定
にするために5分間攪拌を続けた。その間、ジャケット
への蒸気の導入を停止し、1分間通水して若干冷却させ
た。かくして得られた各実施例および比較例の吸水性樹
脂について、ゲル強度を前記と同様にして測定した。そ
の結果を表4に併せて示す。
When the primary treatment products are mixed immediately after drying as in Examples 3, 8 and 9, the same amount of treatment liquid is used as in the comparative examples 7 to 9 in which the primary treatment products are mixed in advance. It can be seen that high gel strength can be obtained with. Further, although the amount of the primary treatment product added in Examples 8 and 9 was higher than that in Example 3, the gel strength was lowered by increasing the amount of the treatment liquid used than that in Example 3. Is prevented. Examples 10-12 and Comparative Examples 10-11 2 kg of the primary treated product obtained in Reference Example was placed in a small stirrer with a jacket (capacity: 10 liters), and the treated liquid (200 g of water, 20 g of diethylene glycol monoethyl ether and ethylene) was stirred. 2 g of glycol diglycidyl ether was mixed and dissolved) was added by spraying, and the mixture was further stirred for 3 minutes. Then, put steam into the jacket of the stirrer so that the water content becomes about 7%,
It was dried at 00 ° C. It took 25 minutes to dry. During these steps, 2 kg of the primary treated product was added at each stage shown in Table 4. After the completion of drying, stirring was continued for 5 minutes in order to keep the conditions of each sample constant. During that time, the introduction of steam into the jacket was stopped, and water was passed for 1 minute to cool it slightly. With respect to the water absorbent resins of the respective Examples and Comparative Examples thus obtained, the gel strength was measured in the same manner as described above. The results are also shown in Table 4.

【0030】[0030]

【表4】 [Table 4]

【0031】表4から、一次処理品の添加時期が乾燥終
了直後のときに最もゲル強度が高く、ついで乾燥開始か
ら20分後、10分後の順になっていることがわかる。 比較例12 比較例1で調製した二次処理品100gを加熱して樹脂
温度を95℃にし、小型攪拌機に入れ、さらに一次処理
品100gを加えて密閉し、5分間攪拌混合した。得ら
れた吸水性樹脂のゲル強度を前記と同様にして測定した
ところ、23000dyn/cm2 であった。
From Table 4, it can be seen that the gel strength is highest immediately after the completion of drying when the primary treatment product is added, and then 20 minutes and 10 minutes after the start of drying. Comparative Example 12 100 g of the secondary treated product prepared in Comparative Example 1 was heated to a resin temperature of 95 ° C., put in a small stirrer, 100 g of the primary treated product was further added, and the mixture was sealed and mixed with stirring for 5 minutes. The gel strength of the obtained water absorbent resin was measured in the same manner as above, and it was 23000 dyn / cm 2 .

【0032】[0032]

【発明の効果】本発明によれば、処理液で処理した吸水
性樹脂粉末に未処理吸水性樹脂粉末を混合するので、吸
水性樹脂粉末の処理量を低減でき、そのため処理の負担
が軽減され、生産性が向上する。また、処理液添加後の
乾燥中または乾燥終了直後に、未処理吸水性樹脂粉末を
添加することにより、得られる吸水性樹脂は充分に実使
用が可能な品質を有しているという効果がある。
According to the present invention, since the untreated water-absorbent resin powder is mixed with the water-absorbent resin powder treated with the treatment liquid, the treatment amount of the water-absorbent resin powder can be reduced and therefore the treatment load is reduced. , Productivity is improved. In addition, by adding untreated water-absorbent resin powder during or immediately after drying after the treatment liquid is added, the resulting water-absorbent resin has an effect that it has a quality that can be sufficiently used in practice. .

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】水、分散剤および架橋剤からなる処理液に
て吸水性樹脂粉末を処理する吸水性樹脂の製造方法にお
いて、前記処理液添加後の乾燥中または乾燥終了直後
に、未処理吸水性樹脂粉末を添加することを特徴とする
吸水性樹脂の製造方法。
1. A method for producing a water-absorbent resin, which comprises treating a water-absorbent resin powder with a treatment liquid comprising water, a dispersant and a cross-linking agent, wherein untreated water absorption is carried out during or after the drying after the treatment liquid is added. A method for producing a water absorbent resin, which comprises adding a water-soluble resin powder.
JP21764793A 1993-09-01 1993-09-01 Method for producing water absorbent resin Expired - Lifetime JP2898180B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21764793A JP2898180B2 (en) 1993-09-01 1993-09-01 Method for producing water absorbent resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21764793A JP2898180B2 (en) 1993-09-01 1993-09-01 Method for producing water absorbent resin

Publications (2)

Publication Number Publication Date
JPH0770228A true JPH0770228A (en) 1995-03-14
JP2898180B2 JP2898180B2 (en) 1999-05-31

Family

ID=16707540

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2898180B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002513043A (en) * 1998-04-28 2002-05-08 エスシーエー・ハイジーン・プロダクツ・アーベー Absorbing structure with improved absorption properties
US9700873B2 (en) 2014-11-27 2017-07-11 Lg Chem, Ltd. Method for preparing super absorbent polymer and super absorbent polymer prepared therefrom

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3700006B1 (en) 2019-02-20 2024-06-05 Luigi Pillosio Multi-purpose device for installing an apparatus on a platform

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002513043A (en) * 1998-04-28 2002-05-08 エスシーエー・ハイジーン・プロダクツ・アーベー Absorbing structure with improved absorption properties
US9700873B2 (en) 2014-11-27 2017-07-11 Lg Chem, Ltd. Method for preparing super absorbent polymer and super absorbent polymer prepared therefrom

Also Published As

Publication number Publication date
JP2898180B2 (en) 1999-05-31

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